EP0234202B1 - Procédé de préparation d'une résine absorbant de l'eau - Google Patents

Procédé de préparation d'une résine absorbant de l'eau Download PDF

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Publication number
EP0234202B1
EP0234202B1 EP87100209A EP87100209A EP0234202B1 EP 0234202 B1 EP0234202 B1 EP 0234202B1 EP 87100209 A EP87100209 A EP 87100209A EP 87100209 A EP87100209 A EP 87100209A EP 0234202 B1 EP0234202 B1 EP 0234202B1
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Prior art keywords
water
process according
polyglycerine
fatty acid
absorbent resin
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EP87100209A
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German (de)
English (en)
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EP0234202A1 (fr
Inventor
Shigeji Obayashi
Morio Nakamura
Takushi Yamamoto
Hitoshi Tanaka
Yuji Sakamoto
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Sumitomo Seika Chemicals Co Ltd
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Seitetsu Kagaku Co Ltd
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/04—Polymerisation in solution
    • C08F2/06—Organic solvent
    • C08F2/08—Organic solvent with the aid of dispersing agents for the polymer
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
    • C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
    • C08F20/04—Acids, Metal salts or ammonium salts thereof
    • C08F20/06—Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L15/00—Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
    • A61L15/16—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
    • A61L15/42—Use of materials characterised by their function or physical properties
    • A61L15/60—Liquid-swellable gel-forming materials, e.g. super-absorbents

Definitions

  • This invention relates to a process for producing a water-absorbent resin. More particularly, the present invention relates to a process for producing a water-absorbent resin having excellent properties as a water-absorbent agent for use particularly in the field of sanitary materials.
  • water-absorbent resins have been used in the field of sanitation as-menstrual articles, diaper, disposable house-cloth and the like, as well as in the field of agriculture and horticulture as water retentive materials and soil improvers. Further, they are useful in other various fields such as coagulation of sludges, prevention of dew condensation on construction materials, dehydration of oils and so on. They have been widely used particularly in the field of sanitation as menstrual articles, diaper, disposable house-cloth and the like. In this case, since they are brought in direct contact with human body, great importance has been placed on the safety of water absorbent-resins.
  • water-absorbent resins In general, requirements for physical properties of water-absorbent resins include water absorbency, water absorption rate, gel strength after water absorption, shape and compatibility with other materials used together. Good water-absorbent resins are those satisfying not only these physical properties but also safety.
  • water-absorbent resins there are known high molecular resins which are crosslinked slightly. Their examples include crosslinked carboxymethyl cellulose, crosslinked polyethylene oxide, crosslinked hydrolyzate of starch-acrylonitrile graft copolymer, crosslinked polyacrylic acid salt and crosslinked vinyl alcohol-acrylic acid salt copolymer.
  • crosslinked hydrolyzate of starch-acrylonitrile graft copolymer has a relatively high water absorbency.
  • it contains starch which is a natural high molecular substance and causes putrefactive decomposition, its storage over a long period of time is difficult. Moreover, its production process is complicated.
  • crosslinked carboxymethyl cellulose and crosslinked polyethylene oxide there has been available no product which has a satisfactory water absorbency.
  • Crosslinked vinyl alcohol-acrylic acid salt copolymer has a relatively high water absorbency.
  • its production process is complicated and causes a high cost.
  • crosslinked acrylic acid salt polymer has a high water absorbency and can be prepared from the starting material, acrylic acid which is readily available commercially, and hence can be produced at a uniform quality and inexpensively, and furthermore causes no putrefaction; thus, crosslinked acrylic acid salt polymer has many advantages and is said to be the most desirable water-absorbent resin.
  • a process for producing a powdery polymer from an a, ⁇ 3-unsaturated carboxylic acid (or a salt thereof) in accordance with inverse emulsion polymerization process or inverse suspension polymerization process is disclosed and known in Japanese Patent Publication No. 10644/1959, Japanese Patent Publication No. 30710/1979, Japanese Patent Application Kokai (Laid-Open) No. 26909/1981, etc.
  • selection of an appropriate surfactant is necessary. This selection is very important with regard to stabilization of W/0 type suspension and control of the particle size of the polymer.
  • sorbitan-fatty acid esters e.g. sorbitan monostearate and sorbitan monopaimitate
  • sorbitol-fatty acid esters e.g. sorbitol monostearate
  • so forth When inverse emulsion polymerization or inverse suspension polymerization is conducted using such a surfactant, the polymer obtained becomes very fine powders having particle diameters as small as 100 to 10 um. Therefore, in handling such powdery polymers, it becomes necessary to set up a countermeasure for dust.
  • Such very fine powders are liable to form unswollen powder lumps when the powders absorb a liquid to be absorbed, resulting in insufficient absorption.
  • a water-absorbent polymer in fine powder form is mixed with or attached to a pulverized pulp, a nonwoven cloth or the like, the polymer is liable to come off therefrom.
  • the present inventors have made an extensive study on a process for stably producing a highly water-absorbent resin which is free from the above mentioned drawbacks of the conventional arts, which has a large average particle diameter, which is high in water absorbency and water absorption rate, and which has a sufficient gel strength and is excellent in safety. As a result, the present invention has been completed.
  • the present inventors have investigated in detail on the production of a water-absorbent resin based on the above mentioned inverse suspension polymerization process and as a result, have found that a highly water-absorbent resin having excellent characteristics as mentioned above can easily be obtained by using a polyglycerine - fatty acid ester as a surfactant. Based on this finding, the present invention has been completed.
  • a polyglycerine - fatty acid ester has no toxicity irrelevently to the molecular weights of the polyglycerine and the fatty acid and, when ingested into human body, is completely decomposed into the polyglycerin and the fatty acid.
  • the polyglycerine is not accumulated in the body and is excreted as it is, together with urine.
  • the fatty acid is absorbed by the body.
  • polyglycerine - fatty acid esters can be used in foods in an unrestricted amount and are actually used widely as a food additive.
  • esters having excellent biodegradability and safety, provide no fear of environmental pollution and phytotoxicity. Furthermore, being unstimulating and protective to human eyes and skin, the polyglycerine - fatty acid esters give no particular problem when water-absorbent resins produced therewith are used in the field of sanitation as articles coming in frequent contact with human body such as diaper, menstrual articles and the like.
  • the present invention provides a process for producing a water-absorbent resin wherein an aqueous solution containing an a,p-unsaturated carboxylic acid and an alkali metal salt thereof in a total amount of 25% by weight or more is subjected to polymerization with a radical polymerization initiator in a petroleum-based hydrocarbon solvent in the presence or absence of a crosslinking agent, characterized by using, as a surfactant, a polyglycerine - fatty acid ester having an HLB of 2 to 16.
  • q, ⁇ -unsaturated carboxylic acid used in the present invention there can be cited acrylic acid and methacrylic acid. If necessary, a part of these acids can be replaced with other polymerizable carboxylic acids such as itaconic acid, crotonic acid, maleic acid, fumaric acid or the like.
  • the alkali metal salt there can be cited salts of sodium, potassium, lithium, etc.
  • the sodium salt is preferably in view of safety because polysodium acrylate is approved as a food additive.
  • the aqueous solution of an a,(3-unsaturated carboxylic acid and of an alkali metal salt thereof which is to be subjected to polymerization is prepared by neutralizing an a,p-unsaturated carboxylic acid with an alkali.
  • the neutralization degree can be varied widely. However, the neutralization degree differs depending upon whether the polymerization for production of a water-absorbent resin is conducted in the absence of a crosslinking agent or in the presence of a crosslinking agent.
  • a self crosslinking reaction In the polymerization in the absence of a crosslinking agent, a self crosslinking reaction must take place during polymerization and a neutralization degree of 40 to 98 mole % is appropriate. When the neutralization degree of 40 to 98 mole % is appropriate. When the neutralization degree is lower than 40 mole %, the self crosslinking reaction takes place to a very high extent, resulting in drastic reduction of water absorbency of the polymer formed. When the neutralization degree exceeds 98 mole %, the majority of the polymer formed becomes water-soluble.
  • the self crosslinking reaction is not necessarily required during polymerization and a neutralization degree of 40 to 100 mole % is appropriate.
  • the neutralization degree is lower than 40 mole %, the water absorbency of the polymer formed is reduced drastically for the reason mentioned above, and the acidity of the polymer increases, which is not desirable in utilization of the polymer.
  • the monomer concentration in the aqueous solution of an a,p-unsaturated carboxylic acid and of an alkali metal salt thereof is preferably from 25% by weight to their saturated solubility point, more preferably from 30% by weight to their saturated solubility point.
  • the monomer concentration is lower than 25% by weight, the majority of the polymer produced in the absence of a crosslinking agent becomes water-soluble and the polymer yield per polymerization reactor is reduced.
  • polymerization can be conducted in the presence or absence of a crosslinking agent.
  • the water-absorbent resin produced in the presence of a crosslinking agent is characterized by having an improved gel strength.
  • the water-absorbent resin of self-crosslinking type produced in the absence of a crosslinking agent is characterized by having high water absorbency.
  • the polymerization conditions can appropriately be selected so as to best meet the application purpose of the water-absorbent resin produced, and the like.
  • a crosslinking agent used in the polymerization in the presence of the crosslinking agent any crosslinking agent can be used as long as it can crosslink a polymer produced from an a,j3-unsaturated carboxylic acid monomer and its alkali metal salt monomer.
  • polymerizable crosslinking agents there can be cited, for example, di- or tri(meth)acrylates of polyols such as ethylene glycol, propylene glycol, trimethylolpropane, glycerine, polyoxyethylene glycol, polyoxypropylene glycol, polyglycerine and the like; unsaturated polyesters obtained by reacting said polyols with unsaturated acids such as maleic acid, fumaric acid and the like; bisacrylamides such as N,N-methylenebisacrylamide and the like; di- or tri(methy)acrylates obtained by reacting a polyepoxide with (meth)acrylic acid; di-(meth)acryloyloethylene carbamates obtained by reacting a polyisocyanate such as tolylene diisocyanate, hexamethylene diisocyanate or the like with hydroxylethyl (meth)acrylate; allylated starch; allylated cellulose; diallyl phthalate; N,N
  • ethylene glycol diacrylate ethylene glycol dimethacrylate, diethylene glycol diacrylate, diethylene glycol dimethacrylate, propylene glycol diacrylate, propylene glycol dimethacrylate, polyethylene glycol diacrylate, polyethylene glycol dimethacrylate, diallyl phthalate, N,N',N"-triallylisocyanurate, N,N'-methylenebisacrylamide, etc.
  • crosslinking agents which react with carboxyl groups present in the a, ⁇ 3-unsaturated carboxylic acid and its a: l sali metal salts or their polymer
  • diglycidyl ether compounds are particularly suitable.
  • Specific examples of the diglycidyl ether compounds include (poly)ethylene glycol diglycidylether, (poly)propylene glycol diglycidyl ether and (poly)glycerine diglycidyl ether. Of these, ethylene glycol diglycidyl ether gives the most preferable effect.
  • haloepoxy compounds include epichlorohydrin, epibromohydrin and a-methylepichlorohydrin.
  • isocyanate compounds include 2,4-tolylenediisocyanate and hexamethylene diisocyanate. All of these crosslinking agents can be used in the present invention.
  • the crosslinking agent is generally used in an amount of 0.001 to 5% by weight, preferably 0.01 to 1 % by weight. When it is used in an amount less than 0.001 % by weight, the water-absorbent resin formed has no improved gel strength after it has absorbed water. When the crosslinking agent is used in an amount more than 5% by weight, the water-absorbent resin formed has remarkably reduced water absorbency, which is not desirable.
  • the petroleum-based hydrocarbon solvent used in the present invention is an aliphatic hydrocarbon, an alicyclic hydrocarbon or an aromatic hydrocarbon.
  • Suitable aliphatic hydrocarbons are n-pentane, n-hexane, n-heptane, ligroin, etc.
  • Suitable alicyclic hydrocarbons are cyclopentane, methylcyclopentane, cyclohexane, methylcyclohexane, etc.
  • Suitable aromatic hydrocarbons are benzene, toluene, xylene, etc.
  • n-hexane, n-heptane, cyclohexane, benzene, toluene and xylene can be used advantageously because they are commercially uniform in quality, easily available and inexpensive.
  • radical polymerization initiator there are properly used radical polymerization initiators generally used, such as potassium persulfate, ammonium persulfate, sodium persulfate and the like. Also, redox initiators which comprise a combination of said initiators and a sulfite or the like, may be used.
  • the radical polymerization initiator is suitably used in an amount of 0.005 to 1.0 mole % based on monomers. When it is used in an amount less than 0.005 mole %, a very long time is required for polymerization. When it is used in an amount more than 1.0 mole %, polymerization takes place suddenly and invites danger.
  • the surfactant used in the polymerization of the present invention can be any polyglycerine - fatty acid ester represented by the general formula
  • the polyglycerine - fatty acid ester is such that the fatty acid component is at least one member selected from lauric acid, palmitic acid, stearic acid, oleic acid and behenic acid.
  • polyglycerine - fatty acid ester examples include diglyceryl monobehenate, diglyceryl monostearate, diglyceryl monolaurate, hexaglyceryl dipalmitate, hexaglyceryl monostearate, hexaglyceryl dioleate, hexaglycerol monobehenate, decaglyceryl pentastearate, decaglyceryl heptastearate, etc.
  • the polyglycerine-fatty acid ester has an HLB of 2 to 16
  • a granular polymer of 100 to 600 ⁇ .1m in particle diameter is obtained.
  • the ester of an HLB less than 2 is used, a stable emulsion can be formed but the polymer obtained becomes lumps.
  • the ester having an HLB more than 16 is used, the ester is difficultly soluble in petroleum-based hydrocarbon solvents and accordingly cannot sufficiently act as a surfactant.
  • the surfactant is suitably used in an amount of 0.05 to 15% ' by weight, preferably 0.1 to 10% by weight based on monomers. When it is used in amount less than 0.05% by weight, the state of stable emulsion cannot be maintained. When it is used in an amount more than 15% by weight, no advantage corresponding to the increased amount can be obtained and such an amount is uneconomical.
  • the polyglycerine - fatty acid ester of the present invention When the polyglycerine - fatty acid ester of the present invention is used as a surfactant, droplets of an aqueous solution of monomers are dispersed uniformly in a solvent; polymerization proceeds more smoothly; and there is obtained a water-absorbent resin. having a uniform and large particle diameter. Further, since the surface of the water-absorbent resin is coated with the polyglycerine - fatty acid ester, agglomeration of particles is prevented; there occurs no adhesion of the polymer to the inner wall of a reactor; and stable operation becomes possible. Furthermore, the following effects are obtained by the use of the present polyglycerine - fatty acid ester as a surfactant.
  • the water-absorbent resin obtained has a fast water absorption rate and excellent water retention. Further, the water-absorbent resin of the present invention has a sufficient gel strength even after it has absorbed water. Therefore, when it is used as a material for sanitation articles such as diaper, sanitary napkin and the like, there is no uncomfortable feeling of wear.
  • water absorbency is a value obtained in accordance with the following procedures. That is, 1 g of a water-absorbent resin was dispersed in 200 ml of a 0.9% aqueous sodium chloride solution and allowed to swell sufficiently. The dispersion was then filtered through a 100 mesh wire gauze. The weight of the swollen resin obtained was measured as the water absorbency of the resin.
  • Water absorption rate was determined as a time required for 1 g of a water-absorbent resin to absorb 30 ml of a 0.9% aqueous sodium chloride solution.
  • a pulp sheet weighing 100 g/m 2 was cutto a size of 40 cm x 10 cm. On one of these cut pulp sheets was uniformly dispersed 3 g of a water-absorbent resin. On the surface of this sheet was superimposed another same pulp sheet. They were pressed by applying the pressure of 1 kg/cm 2 to their entire surfaces whereby an absorbent was formed.
  • the amount of liquid absorbed by the filtering papers was measured to obtain an amount of liquid returned (released).
  • n-heptane Two hundred and eighty ml of n-heptane were placed in a 500 ml, four-necked round bottom flask provided with a stirrer, a reflux condenser, a dropping funnel and a nitrogen-blowing tube. Further, 0.75 g of decaglyceryl pentastearate having an HLB of 3.5 (trade name: Decaglyn 5-S, produced by Nikko Chemical K.K.) was added and dispersed in n-heptane. Nitrogen gas was blown into the flask to remove oxygen dissolved in the dispersion. Then, the temperature of the dispersion was elevated to 50°C to dissolve the surfactant in n-heptane, after which the resulting solution was cooled to 30°C.
  • This aqueous solution of partially neutralized acrylic acid was added into the four-necked flask and dispersed therein.
  • the flask inside was sufficiently purged again with nitrogen and the bath temperature was elevated to 55° to 65°C.
  • the temperature was maintained for 1 hour to conduct polymerization.
  • Water and n-heptane were distilled off and the residue was dried to obtain 40.0 g of a water-absorbent resin having a particle diameter of 200 to 600 pm. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.3 g.
  • Example 2 The procedure of Example 1 was repeated except that the surfactant was changed to hexaglyceryl monobehenate having an HLB of 13.1 (trade name: Nonion GV-106, produced by Nihon Yushi K.K.) and the amount of potassium persulfate was changed to 0.19 g, whereby 40.2 g of a water-absorbent resin having a particle diameter of 150 to 500 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was 0.8 g.
  • Example 1 The procedure of Example 1 was repeated except that the surfactant was changed to diglyceryl monobehenate having an HLB of 7.8 (trade name: Nonion GV-102, produced by Nihon Yushi K.K.), whereby 40.4 g of a water-absorbent resin having a particle diameter of 200 to 600 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.6 g.
  • the surfactant was changed to diglyceryl monobehenate having an HLB of 7.8 (trade name: Nonion GV-102, produced by Nihon Yushi K.K.), whereby 40.4 g of a water-absorbent resin having a particle diameter of 200 to 600 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.6 g.
  • Example 1 The procedure of Example 1 was repeated except that the solvent was changed from n-heptane to toluene, whereby 40.2 g of a water-absorbent resin having a particle diameter of 100 to 350 pm was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was 0.9 g.
  • Example 2 The procedure of Example 1 was repeated except that 0.012 g of ethylene glycol dimethacrylate was added as a crosslinking agent, whereby 40. g g of a water-absorbent resin having a particle diameter of 200 : 0 600 pm was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.2 g.
  • Example 3 The procedure of Example 3 was repeated except that 0.019 g of N,N'-methylenebisacrylamide was added as a crosslinking agent, whereby 40.4 g of a water-absorbent resin having a particle diameter of 200 : 0 600 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was 0.5 g.
  • Example 1 The procedure of Example 1 was repeated except that the surfactant was changed to 2.25 g of decagtyceryl heptastearate having an HLB of 2 (trade name: Decaglyn 7-S, produced by Nikko Chemical K.K.), whereby 41.2 g of a water-absorbent resin having a particle diameter of 200 to 500 pm was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.05 g.
  • Example 3 The procedure of Example 3 was repeated except that the solvent was changed from n-heptane to cyclohexane and 0.038 g of N,N-methylenebisacrylamide was added as a crosslinking agent, whereby 40.0 g of a water-absorbent resin having a particle diameter of 150 to 500 pm was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was 0.7 g.
  • Example 2 The procedure of Example 2 was repeated except that 0.019 g of ethylene glycol diglycidyl ether was added as a crosslinking agent, whereby 40.4 g of a water-absorbent resin having a particle diameter of 150 to 500 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was 0.5 g.
  • Example 2 The procedure of Example 2 was repeated except that 0.012 g of epichlorohydrin was added as a crosslinking agent, wherby 40.5 g of a water-absorbent resin having a particle diameter of 150 to 500 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was 0.7 g.
  • Example 2 The procedure of Example 2 was repeated except that 0.038 g of hexamethylene diisocyanate was added as a crosslinking agent, whereby 40.5 g of a water-absorbent resin having a particle diameter of 150 to 500 pm was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was 0.6 g.
  • Example 5 The procedure of Example 5 was repeated except that 37.5 g of the aqueous solution containing 80% by weight of acrylic acid was changed to 30 g of methacrylic acid and that 49.3 g of the aqueous solution containing 25.4% by weight of sodium hydroxide was changed to 54.1 g of an aqueous solution containing 19.3% by weight of sodium hydroxide, whereby 39.5 g of a water-absorbent resin having a particle diameter of 100 to 400 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was 0.4 g.
  • Example 5 The procedure of Example 5 was repeated except that 63.1 g of an aqueous solution containing 23.7% by weight of sodium hydroxide was added dropwise to neutralize acrylic acid by 90 mole %, whereby 41.5 g of a water-absorbent resin having a particle diameter of 150 to 600 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.3 g.
  • Example 2 The procedure of Example 1 was repeated except that 57.4 g of an aqueous solution containing 32.6% by weight of potassium hydroxide was added dropwise to neutralize acrylic acid by 80 mole %, whereby 45.5 g of a water-absorbent resin having a particle diameter of 150 to 500 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.3 g.
  • Example 2 The procedure of Example 1 was repeated except that 31.7 g of an aqueous solution containing 26.8% by weight of sodium hydroxide was added dropwise to neutralize acrylic acid by 50 mole %, whereby 36.4 g of a water-absorbent resin having a particle diameter of 150 to 500 pm was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.4 g.
  • Example 7 The procedure of Example 7 was repeated except that the amount of potassium persulfate was changed to 0.11 g, whereby 41.0 g of a water-absorbent resin having a particle diameter of 200 to 600 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.1 g.
  • Example 1 The procedure of Example 1 was repeated except that the surfactant was changed to hexaglyceryl dipalmitate having an HLB of 15.8 (trade name: Nonion GP-206, produced by Nihon Yushi K.K.), whereby 40.0 g of a water-absorbent resin having a particle diameter of 100 to 300 pm was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.2 g.
  • Example 2 The procedure of Example 1 was repeated except that the surfactant was changed to hexaglyceryl monolaurate having an HLB of 18.2 (trade name: Nonion GL-106, produced by Nihon Yushi K.K.), whereby 40.8 g of a water-absorbent resin having a particle diameter of 500 to 5,000 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount ofthe polymer which did not pass through a 20 mesh sieve was 37 g.
  • Example 2 The procedure of Example 1 was repeated except that the surfactant was changed to 1.8 g of sorbitan monostearate, whereby 41.8 g of a water-absorbent resin having a particle diameter of 20 to 80 ⁇ m was obtained. There was nothing adhering to the inside wall of the flask and the amount of the polymer which did not pass through a 20 mesh sieve was only 0.3 g.
  • Example 2 The procedure of Example 1 was repeated except that the surfactant was changed to 0.56 g of sorbitan monolaurate and the addition amount of potassium persulfate was changed to 0.19 g, whereby 37.0 g of a water-absorbent resin having a particle diameter of 150 to 500 pm was obtained.
  • the amount of the substance adhering to the inside wall of the flask was 2.0 g and the amount of the polymer which did not pass through a 20 mesh sieve was 1.5 g.
  • Example 2 The procedure of Example 1 was repeated except that the surfactant was changed to 1.8 g of ethyl cellulose (trade name: ETHYL CELLULOSE N-200, produced by Hercules Co.), whereby 26.9 g of a water-absorbent resin having a particle diameter of 100 to 350 pm was obtained.
  • the amount of the substance adhering to the inside wall of the flask was 8.1 g and the amount of the polymer which did not pass through a 20 mesh sieve was 6.5 g.
  • Example 1 The procedure of Example 1 was repeated except that the surfactant was changed to glyceryl monostearate having an HLB of 13.0 (trade name: Monogly, produced by Nihon Yushi K.K). As soon as the polymerization was initiated, the suspension state of the polymerization liquid was destroyed and only lump polymerization product was obtained.
  • the surfactant was changed to glyceryl monostearate having an HLB of 13.0 (trade name: Monogly, produced by Nihon Yushi K.K).

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Claims (13)

1. Procédé pour produire une résine absorbant l'eau, selon lequel une solution aqueuse contenant un acide carboxylique α,β-insaturé et un sel de métal alcalin de celui-ci en une quantité totale de 25% en poids ou plus est soumise à polymérisation au moyen d'un initiateur de polymérisation radicalaire dans un solvant hydrocarboné à base de pétrole en présence ou en l'absence d'un agent réticulant, caractérisé par l'utilisation, en tant qu'agent tensioactif, d'un ester de polyglycérol-acide gras présentant une valeur de HLB (équilibre hydrophile-lypophile) de 2 à 16 et représenté par la formule générale
Figure imgb0005
(dans laquelle R est un groupe acyle ou un atome d'hydrogène et n est un nombre entier de 0 à 8).
2. Procédé selon la revendication 1, dans lequel l'acide carboxylique α,β-insaturé est l'acide acrylique.
3. Procédé selon la revendication 1, dans lequel la concentration molaire du sel de métal alcalin de l'acide carboxylique α,β-insaturé est de 40% ou plus de la quantité totale de l'acide carboxylique α,β-insaturé et de son sel de métal alcalin.
4. Procédé selon la revendication 1, dans lequel le solvant hydrocarboné à base de pétrole est au moins un membre choisi dans le groupe constitué par le n-hexane, le n-heptane, le cyclohexane, le benzène, le toluène et le xylène.
5. Procédé selon la revendication 4, dans lequel le solvant hydrocarboné à base de pétrole est le n-heptane.
6. Procédé selon la revendication 1, dans lequel l'initiateur de polymérisation radicalaire est le persulfate de potassium.
7. Procédé selon la revendication 1, dans lequel l'agent réticulant est le N,N-méthylènebisacrylamide.
8. Procédé selon la revendication 1, dans lequel l'agent réticulant est l'éther diglycidylique de l'éthylène-glycol.
9. Procédé selon la revendication 1, dans lequel l'ester de polyglycérol-acide gras est le mono- béhènate de diglycéryle.
10. Procédé selon la revendication 1, dans lequel l'ester de polyglycérol-acide gras est le mono- béhènate d'hexaglycéryle.
11. Procédé selon la revendication 1, dans lequel l'ester de polyglycérol-acide gras est le pentastéarate de décaglycéryle.
12. Procédé selon la revendication 1, dans lequel l'ester de polyglycérol-acide gras est l'heptastéarate de décaglycéryle.
13. Procédé selon la revendication 1, dans lequel l'ester de polyglycérol-acide gras est utilisé en une quantité de 0,1 à 10% en poids par rapport au poids total de l'acide carboxylique α,β-insaturé et de son sel de métal alcalin.
EP87100209A 1986-01-25 1987-01-09 Procédé de préparation d'une résine absorbant de l'eau Expired - Lifetime EP0234202B1 (fr)

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JP14309/86 1986-01-25
JP61014309A JPH066612B2 (ja) 1986-01-25 1986-01-25 吸水性樹脂の製造法

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EP0234202A1 EP0234202A1 (fr) 1987-09-02
EP0234202B1 true EP0234202B1 (fr) 1990-05-02

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JP (1) JPH066612B2 (fr)
KR (1) KR890004330B1 (fr)
CA (1) CA1282543C (fr)
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AU598894B2 (en) * 1987-02-03 1990-07-05 Nalco Chemical Company Oleic acid as a coemulsifier in water-in-oil latex polymerization
US4833222A (en) * 1987-10-22 1989-05-23 The Dow Chemical Company Crosslinker stabilizer for preparing absorbent polymers
JPH01264803A (ja) * 1988-04-16 1989-10-23 Mitsui Constr Co Ltd コンクリート・モルタル製造用微粒状氷及びドライ状包接水の製造方法及び、それ等微粒状氷又はドライ状包接水を用いたコンクリート・モルタルの製造方法
JP2682007B2 (ja) * 1988-05-20 1997-11-26 三菱化学株式会社 吸水性樹脂を製造する方法
KR930007272B1 (ko) * 1988-06-28 1993-08-04 닙본 쇼쿠바이 가브시기 가이샤 흡수성 수지 및 그 제법
US6087002A (en) * 1988-06-28 2000-07-11 Nippon Shokubai Kagaku Kogyo Co. Ltd. Water absorbent resin
TW201758B (fr) * 1988-06-28 1993-03-11 Catalyst co ltd
JP3040438B2 (ja) * 1990-08-21 2000-05-15 三菱化学株式会社 高吸水性ポリマーの製造法
EP0854154A1 (fr) * 1997-01-16 1998-07-22 Th. Goldschmidt AG Compositions d'émulsifiant
KR100545673B1 (ko) * 1998-06-22 2006-05-23 송원산업주식회사 다공성 흡수성수지의 제조방법
JP3846141B2 (ja) 2000-01-18 2006-11-15 富士ゼロックス株式会社 高分子粒子の製造方法
JP5027414B2 (ja) 2003-03-17 2012-09-19 住友精化株式会社 吸水性樹脂粒子の製造方法
CN101479297B (zh) 2006-04-27 2011-12-21 住友精化株式会社 制造吸水性树脂的方法
JP5439179B2 (ja) 2007-08-23 2014-03-12 住友精化株式会社 衛生材用途に適した吸水性樹脂
WO2011052140A1 (fr) 2009-10-30 2011-05-05 三洋化成工業株式会社 Particules de résine absorbantes utilisées comme agent contre les infiltrations d'eau, et agent contre les infiltrations d'eau contenant ces particules
EP2599796B1 (fr) 2010-07-28 2019-01-23 Sumitomo Seika Chemicals CO. LTD. Procédé de production de résine absorbable par l'eau
KR101778341B1 (ko) 2010-07-28 2017-09-13 스미토모 세이카 가부시키가이샤 흡수성 수지의 제조 방법
CN103003312B (zh) 2010-07-28 2015-05-13 住友精化株式会社 吸水性树脂的制造方法
JP5805639B2 (ja) 2010-07-28 2015-11-04 住友精化株式会社 吸水性樹脂の製造方法
US9061269B2 (en) 2011-02-08 2015-06-23 Sumitomo Seika Chemicals Co., Ltd. Method for producing water-absorbent resin
WO2012176342A1 (fr) 2011-06-24 2012-12-27 住友精化株式会社 Procédé de fabrication d'une résine absorbant l'eau
SG11201507448QA (en) 2013-03-11 2015-10-29 Sumitomo Seika Chemicals Apparatus for producing water-absorbent resin
JP6313280B2 (ja) 2013-03-27 2018-04-18 住友精化株式会社 吸水性樹脂組成物の製造方法
WO2015016075A1 (fr) 2013-07-29 2015-02-05 住友精化株式会社 Procédé de production de particule de résine absorbant l'eau
JP6567503B2 (ja) 2014-03-26 2019-08-28 住友精化株式会社 吸水性樹脂粒子の製造方法
US10124315B2 (en) 2015-02-24 2018-11-13 Sumitomo Seika Chemicals Co., Ltd. Water-absorbent resin production apparatus
JPWO2016158689A1 (ja) 2015-03-30 2018-01-25 住友精化株式会社 包装袋体および包装物品
WO2017169246A1 (fr) 2016-03-31 2017-10-05 住友精化株式会社 Dispositif de production de particules de résine absorbant l'eau

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JPS62172006A (ja) 1987-07-29
KR870007209A (ko) 1987-08-17
DE3762519D1 (de) 1990-06-07
KR890004330B1 (ko) 1989-10-31
ES2014257B3 (es) 1990-07-01
EP0234202A1 (fr) 1987-09-02
CA1282543C (fr) 1991-04-02
JPH066612B2 (ja) 1994-01-26

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